Heat and electric power supply system and operation method thereof

ABSTRACT

A heat and electric power supply system which comprises a regenerative gas turbine and an adsorption refrigerator recovering exhaust heat of exhaust gas from the gas turbine is provided with an inlet air cooling equipment including a spray device for spraying cold water form the adsorption refrigerator into an air-intake port of the regenerative gas turbine and a humidifier effecting humidification by hot water injection from the refirigerator into a compressor delivery port of the regenerative gas turbine. The cooling by cold water and humidification by hot water injection are effected according to operational conditions.

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The present invention relates to a heat and electric power supplysystem which generates and supplies heat and electric power at the sametime and a method of operating the system.

[0003] 2. Description of Prior Art

[0004] A lot of independent (or self-) electric power plants eachoperating a generator using an internal combustion engine or the likehave been proposed as so-called co-generation facilities which generatehot water or steam and cold water by utilizing exhaust heat therefromand supply thermal energy in the form of cold/heat. Some examples ofthem are disclosed in CLEAN ENERGY Vol. 6 No. 12 (1997, issued by JAPANINDUSTRY) at pages 1 to 36. In many of those equipments, a ratio betweenthe maximum quantity electric power which can supply and a cold energyquantity or a heat energy quantity is fixed.

[0005] A cold/heat/electric power supply system which supplies electricpower and thermal energy such as cold/heat at the same time can berealized by a combination of an absorption refrigerator which is made itpossible to supply cold water/hot water at the same time by providing achange-over valve inside for example, and a generator which is driven byan internal combustion engine such as a diesel engine, gas engine, gasturbine or the like. Recently, a small-sized regenerative gas turbineprovided with a regenerative heat exchanger is developed and acold/heat/electric power supply system using such a turbine also is beenstudied.

[0006] An example of a conventional cold/heat/electric power supplysystem is shown in FIG. 8, which employs a generator driven by asmall-sized regenerative gas turbine and an absorption refrigerator. Inthis system, an exhaust gas 7 from the regenerative gas turbine 1 is ledto the absorption refrigerator 2 which recovers heat from the exhaustgas in a regenerator and generates hot water 9 in a condenser and coldwater 8 in an evaporator. In such a system as shown by this example, themaximum power generation output is limited by the maximum output of theregenerative gas turbine and it is impossible to increase the powergeneration output and to increase energy effectively utilized, even inthe case where a demand such as air conditioning has decreased in middleseason whereby a demand of cold/heat has decreased.

[0007] Further, some factors representative of the performance of theconventional system is shown in prior art items of FIG. 2 in the form ofcomparison of power generation efficiency and output between in the casewhere the above-mentioned system is operated in middle season(atmospheric temperature 15° C. and humidity 30%) and in the case wherethe system is operated in summer (atmospheric temperature 38° C. andhumidity 60%). In summer, the air density decreases as the temperatureincreases and a mass flow rate of the air taken in a compressor of theregenerative gas turbine decreases, so that a recovery heat amount in aregenerative heat exchanger of the regenerative gas turbine and turbineoutput decrease and both the power generation terminal output and powergeneration efficiency change greatly, as shown in FIG. 2.

SUMMARY OF THE INVENTION

[0008] The present invention is made in view of the above-mentionedpoints, and an object of the present invention is to provide a heat andelectric power supply system and an operation method thereof whichenables the power generation output to increase.

[0009] In order to attain the above-mentioned object, a heat andelectric power supply system according to the present inventioncomprises gas turbine equipment generating electric power, absorptionrefrigerating equipment recovering exhaust heat from the gas turbineequipment and generating thermal energy, and air cooling equipmentfluidly connected to the gas turbine and the absorption refrigeratingequipment and cooling air for power generation in the gas turbineequipment with the thermal energy generated in the absorptionrefrigerating equipment. An example of the air cooling equipment is aspray device for spraying cold water from the absorption refrigeratoronto the air to be taken in a compressor of the regenerative gas turbineor a humidifier for humidifying the air from the compressor with hotwater from the absorption refrigerator. The system can be provided witha heat recovering device for recovering heat from exhaust gas of theadsorption refrigerator and/or an accumulation type heat exchanger forrecovering accumulating heat from exhaust gas of the adsorptionrefrigerator.

[0010] Further, in order to attain the above-mentioned object, accordingto the present invention, the operation method of a heat and electricpower supply system which comprises gas turbine equipment and absorptionrefrigerating equipment recovering exhaust heat of the gas turbineequipment cooling or heating water, is characterized in that intake airof the gas turbine equipment is cooled by spraying or injecting thewater generated in the absorption refrigerator onto the intake air. Anexample of the water used for cooling the intake water is at least oneof cold water and hot water.

BRIEF DESCRIPTION OF THE DRAWINGS

[0011]FIG. 1 is a schematic diagram of construction of acold/heat/electric power supply system employing a regenerative gasturbine and an absorption refrigerator, of an embodiment of the presentinvention;

[0012]FIG. 2 is a graph showing comparison of power generationefficiency and power generation output between in the case where aconventional system used in middle season, in the case where electricoutput is increased by applying a method of an embodiment of the presentinvention in a cold/heat/electric power supply system and in the casewhere the conventional method is used in summer;

[0013]FIG. 3 is a graph showing a compressor power, regenerative heatexchanging amount and gas turbine output in summer, in middle season inthe case where electric output is increased in cold/heat/electric powersupply systems according to an embodiment of the present invention andaccording to a prior art, respectively;

[0014]FIG. 4 is a schematic diagram of a construction of acold/heat/electric power supply system of another embodiment of thepresent invention;

[0015]FIG. 5 is a schematic diagram of a construction of acold/heat/electric power supply system of another embodiment of thepresent invention;

[0016]FIG. 6 is a schematic diagram of a construction of acold/heat/electric power supply system of another embodiment of thepresent invention;

[0017]FIG. 7 is a schematic diagram of a construction of acold/heat/electric power supply system of another embodiment of thepresent invention; and

[0018]FIG. 8 is a schematic diagram of a conventional construction of acold/heat/electric power supply system employing a regenerative gasturbine and an absorption refrigerator.

DESCRIPTION OF EMBODIMENTS OF THE INVENTION

[0019] A heat and electric power supply system (cold/heat/electric powerequipment), that is, a system or equipment which is able to jointlysupply thermal energy (cold and heat) and electric power, of eachembodiment of the present invention relates to a so-called co-generationsystem. The co-generation system is provided with an electric powergenerating function to supply electric power to a demandant such as ahouse, glass culture farm house, small-sized factory, each section ofcollective houses, hospital, hotel, combined sport facilities, or thelike, and supplies cold energy and heat energy to facilities such as airconditioning equipment. Particularly, a system which employs aregenerative gas turbine as a motor will be described hereunder.

[0020] A cold/heat/electric power supply system of an embodiment of thepresent invention will be described hereunder, referring to FIG. 1. FIG.1 shows the cold/heat/electric power supply system provided with aregenerative gas turbine 1 driving a generator 16, and an absorptionrefrigerator 2 supplied with water through a feed water treatingapparatus 30 and supplying a demandant such as an air conditioningapparatus or the like with cold water 8 and hot water 9. Further, thesystem and its operation will be described in detail, referring to FIG.1.

[0021] A spray device 31 for intake air is provided at an inlet of theregenerative gas turbine 1. The spray device 31 sprays cold water ontothe air 3 taken in the gas turbine 1 to humidify and cool the airaccording to the circumference and operation conditions. The air takenin, that is, intake air is compressed by a compressor 11 and led to ahumidifier 12. In the humidifier 12, hot water of necessary quantity issprayed according to operation conditions such as power demand or thelike and able to humidify the intake air. The intake air exiting fromthe humidifier 12 is led into a regenerative heat exchanger 13 in whichthe intake air recovers the heat of exhaust gas from a turbine 15 and ispreheated thereby. The preheated intake air is mixed with fuel 4 in acombustor 14 and the mixture is burnt therein and flows into the turbine15 as a high temperature gas. In the turbine 15, the high temperaturegas expands to work, whereby output is obtained. The output drives thecompressor 11 and the generator 16. The exhaust gas exiting from theturbine 15 is led into a regenerator 21 of the absorption refrigerator 2as gas turbine exhaust gas 70 after the heat of the exhaust gas has beenrecovered in the regenerative heat exchanger 13. In the regenerator 21,the heat of the turbine exhaust gas 70 is recovered and finallyexhausted out of the system as absorption refrigerator exhaust gas 71.

[0022] In the absorption refrigerator 2, the regenerator 21 recoversheat from the gas turbine exhaust gas 70 and evaporates a solvent from adilute solution 29 to generate vapor 28. The vapor 28 generated in theregenerator is led to a condenser 22. The absorption refrigerator 2 hasequipments for supplying feed water 50 from outside the equipment astreatment-finished feed water 51 by a feed pump 25 after treatment suchas dust removal, water softening or the like is effected in the eedwater treating apparatus 30, and is constructed so that water can becompensated by the amount of water consumed by the demandant or in theregenerative gas turbine 1. The feed water treating apparatus 30 isconstructed so that the condensate 52 exhausted and recovered from ademandant such as air conditioning apparatus or the like also can bejointly supplied in addition to the feed water 50 from outside.

[0023] The supplemented treatment-finished water 51 and the water whichis circulated by a recirculation pump 24 inside the absorptionrefrigerator 2 cool the vapor 28 in the condenser 22 and receive therebyheat from the vapor to turn into hot water 9. The generated hot water 9is led to an evaporator 23 after the hot water of a quantity necessaryfor a demandant and the regenerative gas turbine 1 is branched by a hotwater bypass valve 26 provided inside the absorption refrigerator 2. Theinside pressure of the evaporator 23 is reduced to be about vacuum andthe solvent condensed in the condenser 22 evaporates due to reducedpressure and is turned into vapor 28 again. In this case, latent heat istaken out from the hot water 9, whereby water exiting from theevaporator 23 becomes cold water 8. The vapor generated in theevaporator 23 is led to an absorber 20 and absorbed in a solutionconcentrated in the regenerator 21 thereby to become a dilute solution29. The dilute solution 29 is sent to the regenerator 21. The cold water8 generated in the evaporator 23 is recirculated by an optimum quantityregulated by a cold water bypass valve 27 according to the operationconditions inside the absorption refrigerator 2, and then the remainingcold water is taken out of the absorption refrigerator 2 and supplied toa demandant such as an air conditioning apparatus or the like or to theregenerative gas turbine 1 through a branch valve 33.

[0024] Next, in the cold/heat/electric power supply system of thepresent embodiment, in the case where the absorption refrigerator 2generates cold/heat in excess, an operation (control) method ofsupplying the excess heat quantity to the regenerative gas turbine 1 andimproving thereby the electric power output and power generationefficiency will be explained.

[0025] In the cold/heat/electric power system of construction asmentioned above, a supply ratio of cold water/hot water can be setfreely by regulating the opening of each of the hot water bypass valve26 and cold water bypass valve 27, so that in the case where any of coldwater and hot water is generated in excess, the excess heat can be takenin any form such as cold water or hot water. In the case where it issufficient to be small in excess heat and in increment of powergeneration terminal output, the excess heat is taken out as cold water,and the cold water branch valve 33 is opened and gas turbine supply coldwater 80 is supplied to the spray device 31 for intake air through acold water feed pump 34 to humidify and cool the intake air by spraywater 81 for intake air, whereby it is effective to reduce powernecessary for the compressor by reducing a thermal drop in thecompressor of the regenerative gas turbine and improve the powergeneration terminal output and power generation efficiency. Further,since a mass flow increases by the humidification, the effect becomelarge without greatly decreasing the intake air temperature, as aresult, there is an advantage that only very small amount of cold wateris consumed.

[0026] The spray water 81 for intake air can attain a reducing effect ofthe compressor power through a change in specific heat ratio due tohumidification even if the spray water 81 is sprayed at a very smallflow rate such as about 0.01 wt % of the air mass flow rate. By sprayingwater of a slight amount about 0.01 wt % of the air flow rate, theintake air of the regenerative gas turbine 1 is humidified to an extentthat the intake air reaches the saturated steam pressure. A temperaturedecrease in the intake air by this humidification is about 0.2° C. orso, however, the compressor efficiency is improved 0.4 to 0.5% atrelative value by decrease in specific heat ratio, and about 1.2% of thecompressor power can be reduced. Additionally, in order to surelyevaporate the spray water 81 for intake air and rapidly humidify theintake air to the saturated condition, a flow rate of water of about 0.2wt % of the air mass flow rate is optimum. In this case, of cold waterdroplets which have reached a state of equilibrium but have notevaporated as yet under the saturated condition, large diameter dropletsare discharged out and recovered as drain, and fine droplets aredelivered through the compressor 11 together with the intake air andevaporate at the delivery port, whereby the same effect as water of avery small quantity has been humidified by the humidifier 12 can beattained.

[0027] For example, when cold water of 0.2 wt % of an intake air massflow rate is used as spray water 81 for humidifying and cooling theintake air, about 3.4% of the power generation output and about 2.9% ofpower generation efficiency are improved. In the case where furtherexcess heat exists, the excess heat is taken out as hot water, that is,the hot water branch valve 37 is opened and branch hot water 90 is sentto the humidifier 12 by a hot water pump 38 and sprayed as supply hotwater 91 by the humidifier 12, whereby the power generation output andpower generation efficiency each are improved further greatly. When thisoperation is taken, it is more effective to increase a fuel flow rateand raise a little a set temperature at the turbine inlet. The reason isthat because of latent heat taken when the hot water supplied by thehumidification evaporates, there are brought about an effect that thephenomenon that the air temperature is lowered at the inlet of thecombustor is damped irrespective of increase of a regenerative heatexchanging amount and an effect that it is avoided to become unstable incombustion under the condition that a lot of steam exists. Further, inthis case, even if a turbine inlet temperature (combustion temperature)is raised, a lot of steam exists in the combustion place, so thatemission of nitrogen oxides (NO_(x)) does not increase.

[0028] In Table 1, there is shown an operation example in which theexcess heat is taken out as cold water and hot water, intake air isspray-cooled and humidified at the compressor delivery port, whereby thepower generation output and power generation efficiency are improved. Inthe example, a cold/heat/electric power supply system is used, whichemploys a regenerative gas turbine-driven generator of rated revolutionof 65,000 rpm having a generation output of 75 kW under the conditionthat the surrounding air temperature is 15° C. and the relative humidityis 30%. TABLE 1 Items Prior art Embodiment Effect (rel. %) Powergeneration output (kW) 75 90 +20.2%  Power generation (%) 29.9% 32.8%+9.6% terminal efficiency R.P.M. (rpm) 65000 — Compression ratio (—) 4.0— Compressor efficiency (%) 79.0% 79.5% +0.5% Turbine efficiency (%)82.1% 81.8% −0.3% Inlet air temp. ° C. 15.0 14.8 — Regenerator inlettemp. ° C. 191 144 — Combustor inlet temp. ° C. 616 610 — Turbine inlettemp. ° C. 930 950 — Exhaust gas temp. ° C. 256 204 — Compressor power(kW) 120 118 −1.2% Turbine output (kW) 214 232 +8.2% Regenerative heat(kW) 306 382 +24.9%  exchanging amount

[0029] In Table 1, a row of a prior art shows results in the case wherethe operation method of improving electricity output and powergeneration efficiency according to the present embodiment is not taken.A row of the present embodiment shows results in the case where theoperation method of improving electricity output and power generationefficiency according to the present embodiment is taken. A row ofeffects shows, by relative values (%) to the prior art, the results inthe case where the operation method of the present embodiment isapplied. In the operation example shown in Table 1, cold water of 7° C.is supplied at a flow rate 0.2 wt % of an air flow rate as spray waterfor intake air, and hot water of 80° C. is supplied at flow rate of 3 wt% of the air flow rate as humidification water. 50% of the spray waterfor intake air is discharged as drain and recovered. Further, in orderto secure the stability of combustion, the turbine inlet temperature(combustion temperature) is raised by 20° C.

[0030] As a result, as shown in Table 1, 0.5% of the compressorefficiency is improved by spraying onto intake air and 1.2% of thecompressor power is reduced. Further, a regenerative heat exchangingamount is increased about 25% by an effect of humidification and theturbine output is increased by about 8%. The reason that the turbineefficiency is decreased by 0.3% is that the specific heat ratiodecreases by the humidification, however, the regenerative heatexchanging amount increases greatly, so that the decrease of the turbineefficiency does not cause a bad influence.

[0031] Next, in the cold/heat/electric power supply system shown in FIG.1, an effect of damping the decrease of power generation output andpower generation efficiency of the regenerative gas turbine in summer inthe case where the method according to the present invention is usedwill be described.

[0032] In summer as mentioned above, air density decreases according toincrease of the atmospheric temperature, whereby a mass flow rate of theair taken in the compressor 11 decreases and the power generation outputand power generation efficiency decreases. However, in thecold/heat/electric power supply system of construction having thehumidifier 12 and spray device 31 for intake air as shown in FIG. 3,humidification and cooling by cold water and humidification by hotwater, as mentioned above are effected, whereby it is possible to notonly damp the decrease of the power generation output and powergeneration efficiency but rather to improve them.

[0033] In the present embodiment, provided is the humidifier 12 forinjecting hot water generated in the absorption regenerator 2 onto theair delivered from the compressor 11 of the regenerative gas turbine 1and humidifying greatly the air to be supplied to the regenerative heatexchanger 13, combustor 14 and turbine 15. Although humidification ofthe air also can be effected by the above-mentioned spray device 31 forintake air, an atmospheric temperature is about 40° C. at highest andatmospheric pressure also is about 100 kPa and low in the case of use ofthe spray device 31, so that saturated steam pressure is low and it cannot be desired to humidify greatly by the spray device 31. However, theair delivered from the compressor 11 has been raised in temperature andpressure by compression of the air in the compressor 11, so that it ispossible to humidify greatly. For example, even in the case where aregenerative gas turbine of relatively small size such that acompression ratio is about 3.5 to 4 or so is supposed, it is possible toeffect humidification with hot water of about 1 wt % of the air flowrate until the air reaches the saturated state. Further, it isunnecessary that all the supplied water has evaporated within thehumidifier, and since any problems do not occur on operation ofapparatuses unless finally any bad affection due to water droplets isimparted on the combustor and turbine, more humidification is possible.

[0034] Further, in the heat and electric power supply equipment with thehumidifier 12 of the present embodiment, by humidifying the air to besupplied to the turbine with a lot of water, an effect of improvement ofthe heat transfer efficiency other than increase in mass flow rate inthe regenerative heat exchanger 13, an effect of suppression of nitrogenoxides (NO_(x)) due to existence of steam in the combustor 14 and aneffect of increase in output due to increase in mass flow rate in theturbine 15 each can be expected. For example, in the case wherehumidification is effected with 3 wt % of an air flow rate in thehumidifier 12, in the regenerative heat exchanger 13, since (1) aneffective temperature difference due to decrease in air temperature atthe regenerative heat exchanger inlet expands, (2) the heat transferefficiency due to mixture of steam with the air is raised and (3) thelatent heat of water flowing into the regenerative heat exchanger asliquid droplets also is contributed to a heat amount regenerated, aregenerative heat exchanging amount increases about 20%, the turbineoutput also increases about 7% at relative value and the powergeneration terminal output and power generation efficiency each areimproved greatly.

[0035]FIG. 2 shows, in a cold/heat/electric power supply system using aregenerative gas turbine-driven generator of rated revolutions of 65,000rpm and power generation output of 75 kW taken as an example in Table 1,comparison between the power generation terminal efficiency and powergeneration output (prior art in middle season) under the operationcondition of ambient air temperature 15° C. and relative humidity 30%,power generation terminal efficiency and power generation output underthe operation condition of ambient air temperature 38° C. and relativehumidity 60% as a representative operation condition (prior art insummer), and power generation terminal efficiency and power generationoutput (present embodiment in summer) in the case where thehumidification and cooling by cold water and the humidification by hotwater according to the operation method of the present embodiment areused. Here, also, the results under the operation conditions that coldwater of 7° C. is supplied at a flow rate of 0.2 wt % of the air flowrate as spray water for intake air and hot water of 80° C. is suppliedat a flow rate of 3 wt % of the air flow rate as water forhumidification are shown as an example. 50% of the spray water forintake air was exhausted and recovered as drain water. Further, in orderto secure the stability of combustion, a turbine inlet temperature(combustion temperature) was raised by 20° C.

[0036] In the conventional cold/heat/electric power supply system, thepower generation output and power generation efficiency decrease about11% and about 16%, respectively, in summer because of decrease in airmass flow rate. However, in the case where the operation method of thepresent embodiment is used, the power generation output and powergeneration efficiency are improved by about 12% and about 10%,respectively. For more detailed explanation of the effects, FIG. 3 showscompressor power, regenerative heat exchanging amount and turbine outputunder each operation condition shown in FIG. 2.

[0037] In the prior art, in middle season and summer the compressorpower does not almost change, but, the regenerative heat exchangingamount decreases greatly because of decrease in air mass flow rate, andthe turbine output decreases also. However, when the present embodimentis used, the mass flow rate is increased by humidification and theregenerative heat exchanging amount is increased greatly by latent heatof hot water supplied for humidification, whereby the regenerative heatexchanging amount is large even in summer and the turbine output also islarge compared with that in the middle season by the prior art in whichhumidification is not effected. Thereby, when the construction andoperation method of the present embodiment as mentioned above areemployed, it is possible to improve the power generation output andpower generation efficiency even in summer.

[0038]FIG. 4 shows a cold/heat/electric power supply system of anotherembodiment of the present invention. The same constructions as in FIG. 1are omitted to explain here, again. In the present embodiment, in orderto further raise the improving effects of power generation output andpower generation efficiency in summer, an intake air cooling device 32for cooling the inlet air by heat exchange between cold water and theintake air is provided upstream of the spraying device 31 for intakeair. The intake air cooling device 32 can supply inlet air cooling water82 through an inlet air cooling device flow adjusting valve 36 in such acases that excess cooling water is generated, an ambient temperature isparticularly high in summer, and so on. Intake air cooling water 53 fromthe intake air cooling device 32 is recovered in an inlet of the feedwater treating device 30 and circulates inside the cold/heat/electricpower supply system.

[0039]FIG. 5 shows a cold/heat/electric power supply system of anotherembodiment of the present invention. The same constructions as mentionedabove are omitted to explain further. In the present embodiment, a waterrecovery device 40 is added to the construction of the embodiment shownin FIG. 4. That is, in the present embodiment, the water recovery device40 for recovering water in the absorption refrigerator exhaust gas 71exhausted from the absorption refrigerator 2 (regenerator 21) isprovided. When operation control of spraying over the intake air andhumidification of compressor delivery air is carried out by employingthe present embodiment, water of several % of the intake air mass flowrate is consumed, so that in some cases a lot of water is included inthe absorption refrigerator exhaust gas 71. The water recovery device 40is provided for recovering the water from the absorption refrigeratorexhaust gas 71 and effectively using the water as cleaning water or thelike. A part of the intake air cooling water 53 led from the intake aircooling device 32 is branched by a water recovering flow adjusting valve41 and sprayed as a water recovery device spray water 54 into the waterrecovery device 40, whereby direct heat exchange is effected and thewater in the exhaust gas 71 is recovered.

[0040] According to this recovering method, it is possible to recovermost of the water in the exhaust gas 71 without greatly increasingexhaust gas pressure loss, however, it also is possible to provide awater recovery device of heat exchanger type which uses the intake aircooling water 53 as a cooling water. The recovery water 55 recovered inthe water recovery device 40 is subjected to dust removal or pHadjustment by a recovery water treatment device 42 and used astreatment-finished recovery water 56. The treatment-finished recoverywater is suitable for use as cleaning water in various equipments.

[0041]FIG. 6 shows a cold/heat/electric power supply system of anotherembodiment of the present invention. The same constructions as mentionedabove are omitted to explain further. In the present embodiment, a heataccumulation type heat exchanger 39 is added to the construction of theembodiment shown in FIG. 5. That is, in the present embodiment, the heataccumulation type heat exchanger 39 is provided for causing theabsorption refrigerator exhaust gas 71 exhausted from the absorptionrefrigerator 2 (regenerator 21) to heat-exchange with feed water 50. Theheat exchanger exhaust gas 72 cooled in the heat accumulation type heatexchanger 39 is led to the water recovery device 40 to recover water inthe exhaust gas. Further, the feed water heated through heat exchangewith the absorption refrigerator exhaust gas 71 in the heat accumulationtype heat exchanger 39 is supplied to hot water-utilizing apparatusesnot shown as hot water 9.

[0042] Generally, the absorption refrigerator exhaust gas 71 is stillkept hot 120° C. or more even after exhaust heat is recovered, and theheat of the exhaust gas 71 is wasted out of the system. However, even ifit is tried to effectively use the heat, since a temperature drop issmall, an amount of hot water generated thereby does not become large,and economical advantages are small by an amount corresponding to anincrease in mechanical complexity. Therefore, in the present embodimentshown in FIG. 6, as mentioned above, such a construction is taken thatthe heat accumulation type heat exchanger 39 is provided in an exhaustpath of the absorption refrigerator 2, the heat from exhaust heat of theabsorption refrigerator exhaust gas 71 is recovered and accumulated, andhot water is generated by supplying the feed water 50 to the heataccumulation type heat exchanger 39 when a demand of hot water becomeslarge.

[0043] In this manner, the exhaust heat is accumulated and recovered togenerate hot water according to a demand, whereby it is possible tofurther improve the efficiency of exhaust heat recovery and use.Further, in the present embodiment shown in FIG. 6, recovery water 55from the water recovering device 40 is subjected to dust removal or pHadjustment in the recovery water treatment device 42, and returned intoa supply port of the feed water treatment device 30 astreatment-finished water 56, whereby an recirculation amount of waterwithin the cold/heat/electric power supply equipment is increased and afeed water amount to the equipments is reduced.

[0044]FIG. 7 shows a cold/heat/electric power supply system of anotherembodiment of the present invention. The same constructions as mentionedabove are omitted to explain further. In the present embodiment, wateris not supplied to the heat accumulation type heat exchanger as feedwater 50 as in the construction of the embodiment shown in FIG. 6, butsteam 10 is generated by using the hot water 9 generated in theabsorption refrigerator 2. By recovering exhaust heat by the heataccumulation type heat exchanger 39 as mentioned above, it is possibleto recover and accumulate the exhaust heat corresponding to the capacityof the heat accumulation type heat exchanger 39 as long as it is notrequired, and it also is possible to discharge all of it at a timethereby to generate steam 10 from the hot water 9. In some cases, steamfor sterilization is intermittently necessary in food factories or thelike. The system as shown in FIG. 7 is suitable for such use.

[0045] As has been explained above, in the heat and electric powersupply system of the present embodiment, a heat/electricityratio-variable operation which could not be effected by a conventionalcold/heat/electric power supply system, that is, an operation whichsupplies excess heat to the regenerative gas turbine and improves thepower generation output and power generation efficiency when excesscold/heat is generated in the absorption refrigerator can be carriedout. Further, in the present embodiment, it is possible to improve, byusing a part of the cold/heat generated in the absorption refrigerator,the characteristics that the power generation terminal output and powergeneration efficiency decreases due to an decrease in air density causedby rising in ambient temperature in summer.

[0046] According to the present invention, it is possible to provide aheat and electric power supply system and an operation method thereofwhich enable the power generation output to increase.

What is claimed is:
 1. A heat and electric power supply systemcomprising: gas turbine equipment generating electric power; absorptionrefrigerating equipment recovering exhaust heat from said gas turbineequipment and generating thermal energy; and air cooling equipment,fluidly connected to said gas turbine and said absorption refrigeratingequipment and cooling air for power generation in said gas turbineequipment with the thermal energy generated in said absorptionrefrigerating equipment.
 2. A heat and electric power supply systemaccording to claim 1 , wherein said thermal energy is used for coolingthe air in the form of cold water and/or hot water.
 3. A heat andelectric power supply system according to claim 2 , wherein said coolingequipment comprises at least one of a spray device for spraying coldwater from said absorption regenerating equipment onto air to be takenin a compressor of said gas turbine equipment, a humidifier forhumidifying air at a delivery side of said compressor with hot waterfrom said absorption regenerating equipment and an air cooling devicedisposed upstream of said spray device for cooling air to be taken insaid compressor.
 4. A heat and electric power supply system according toclaim 2 , wherein a water recovering device is provided for recoveringwater contained in the exhaust gas having passed through said absorptionrefrigerating equipment.
 5. A heat and electric power supply systemaccording to claim 2 , wherein a heat accumulation type heat exchangeris provided for recovering and accumulating exhaust heat from exhaustgas having passed through said absorption refrigerating equipment.
 6. Aheat and electric power supply system comprising: gas turbine equipment;absorption refrigerating equipment recovering exhaust heat from said gasturbine equipment and cooling or heating water; and an air coolingdevice leading water cooled in said absorption refrigerating equipmentand cooling intake air of said gas turbine equipment.
 7. A heat andelectric power supply system comprising: gas turbine equipment,absorption refrigerating equipment recovering exhaust heat of said gasturbine equipment and cooling or heating water, and a spraying devicefor intake air, spraying water cooled in said absorption refrigeratingequipment onto intake air of said gas turbine equipment.
 8. A heat andelectric power supply system comprising: gas turbine equipment having acompressor for compressing air, a combustor for burning compressed airand fuel, a turbine driven by combustion gas generated in saidcombustor, and a regenerative heat exchanger for heat-exchanging exhaustgas from said turbine and compressed air led to said combustor;absorption refrigerating equipment for recovering exhaust heat of saidgas turbine equipment and cooling or heating water; and a humidifierspraying water heated in said absorption regenerating equipment onto thecompressed air in said compressor.
 9. A heat and electric power supplysystem comprising: gas turbine equipment generating electric power bydriving a generator; absorption refrigerating equipment recoveringexhaust heat of said gas turbine equipment and generating cold water orhot water; an air cooling device cooling intake air of said gas turbineby using water generated in said absorption refrigerating equipment; anda humidifier spraying hot water generated in said absorptionregenerating equipment and humidifying turbine intake air.
 10. A heatand electric power supply system according to claim 6 , wherein saidheat and electric power supply equipment is provided with a waterrecovering device for recovering water contained in the exhaust gashaving passed through said absorption refrigerating equipment.
 11. Aheat and electric power supply system according to claim 6 , whereinsaid heat and electric power supply equipment is provided with a heataccumulation type heat exchanger for recovering and accumulating exhaustheat from exhaust gas having passed through said absorptionrefrigerating equipment.
 12. An operation method of a heat and electricpower supply system comprising gas turbine equipment and absorptionrefrigerating equipment recovering exhaust heat of said gas turbineequipment and cooling or heating water, wherein in the case where coldor heat generated in said absorption refrigerating equipment have beenexcess, the excess heat is supplied to said gas turbine equipment. 13.An operation method of a heat and electric power supply systemcomprising gas turbine equipment and absorption refrigerating equipmentrecovering exhaust heat of said gas turbine equipment and cooling orheating water, wherein intake air is cooled by spraying water cooled insaid absorption refrigerating equipment onto the intake air of said gasturbine equipment.
 14. An operation method of a heat and electric powersupply system comprising gas turbine equipment and absorptionrefrigerating equipment recovering exhaust heat of said gas turbineequipment and cooling or heating water, characterized in that compressedair of said gas turbine equipment is humidified by spraying thereonwater heated in said absorption refrigerating equipment.
 15. Anoperation method of a heat and electric power supply system comprisinggas turbine equipment driving a generator and generating electric powerand absorption refrigerating equipment recovering exhaust heat of saidgas turbine equipment and generating cold water or hot water, whereingas turbine intake air is cooled by using cold water generated in saidabsorption refrigerating equipment and humidified by spraying thereonhot water generated in said absorption refrigerating equipment.
 16. Anoperation method of a heat and electric power supply system according toclaim 12 , wherein said operation method of heat and electric powersupply equipment recovers and accumulates exhaust heat form exhaust gaspassed through said absorption refrigerating equipment, and hot water isgenerated from the accumulated exhaust heat when the hot water isrequired.
 17. An operation method of a heat and electric power supplysystem according to claim 14 , characterized in that said operationmethod of heat and electric power supply equipment a fuel flow rate tobe supplied into a combustor of said gas turbine equipment is increasedwhen humidification is effected.